cover
Contact Name
Himawan Tri Bayu Murti Petrus
Contact Email
jurnal.rekpros@ugm.ac.id
Phone
-
Journal Mail Official
jurnal.rekpros@ugm.ac.id
Editorial Address
Jl. Grafika No. 2, Yogyakarta, Indonesia
Location
Kab. sleman,
Daerah istimewa yogyakarta
INDONESIA
Jurnal Rekayasa Proses
ISSN : 1978287X     EISSN : 25491490     DOI : -
Core Subject : Engineering,
Jurnal Rekayasa Proses is an open-access journal published by Chemical Engineering Department, Faculty of Engineering, Universitas Gadjah Mada as scientific journal to accommodate current topics related to chemical and biochemical process exploration and optimization which covers multi scale analysis from micro to macro and full plant size. Specialization topics covered by Jurnal Rekayasa Proses are: 1. Kinetics and Catalysis Includes simulations and experiments in reaction kinetics, catalyst synthesis and characterization, reactor design, process intensification, microreactor, multiphase reactors, multiscale phenomena, transfer phenomena in multiphase reactors. 2. Separation and Purification System Includes phase equilibrium, mass transfer, mixing and segregation, unit operation, distillation, absorption, extraction, membrane separation, adsorption, ion exchange, chromatography, crystallization and precipitation, supercritical fluids, bioprocess product purification. 3. Process System Engineering Includes simulation, analysis, optimization, and process control on chemical/biochemical processes based on mathematical modeling; multiscale modeling strategy (molecular level, phase level, unit level, and inter-unit integration); design of experiment (DoE); current methods on simulation for model parameter determination. 4. Oil, Gas, and Coal Technology Includes chemical engineering application on process optimization to achieve utmost efficiency in energy usage, natural gas purification, fractionation recovery, CO2 capture, coal liquefaction, enhanced oil recovery and current technology to deal with scarcity in fossil fuels and its environmental impacts. 5. Particle Technology Includes application of chemical engineering concepts on particulate system, which covers phenomenological study on nucleation, particle growth, breakage, and aggregation, particle population dynamic model, particulate fluid dynamic in chemical processes, characterization and engineering of particulate system. 6. Mineral Process Engineering Includes application of chemical engineering concepts in mineral ore processing, liberation techniques and purification, pyrometallurgy, hydrometallurgy, and energy efficiency in mineral processing industries. 7. Material and biomaterial Includes application of chemical engineering concepts in material synthesis, characterization, design and scale up of nano material synthesis, multiphase phenomena, material modifications (thin film, porous materials etc), contemporary synthesis techniques (such as chemical vapor deposition, hydrothermal synthesis, colloidal synthesis, nucleation mechanism and growth, nano particle dispersion stability, etc.). 8. Bioresource and Biomass Engineering Includes natural product processing to create higher economic value through purification and conversion techniques (such as natural dye, herbal supplements, dietary fibers, edible oils, etc), energy generation from biomass, life cycle and economic analysis on bioresource utilization. 9. Biochemistry and Bioprocess Engineering Includes biochemical reaction engineering, bioprocess optimization which includes microorganism selection and maintenance, bioprocess application for waste treatment, bioreactor modeling and optimization, downstream processing. 10. Biomedical Engineering Includes enhancement of cellular productions of enzymes, protein engineering, tissue engineering, materials for implants, and new materials to improve drug delivery system. 11. Energy, Water, Environment, and Sustainability Includes energy balances/audits in industries, energy conversion systems, energy storage and distribution system, water quality, water treatment, water quality analysis, green processes, waste minimization, environment remediation, and environment protection efforts (organic fertilizer production and application, biopesticides, etc.).
Articles 5 Documents
Search results for , issue "Vol 6 No 2 (2012): Volume 6, Number 2, 2012" : 5 Documents clear
Studi simulasi pada unit reformer primer di PT Pupuk Sriwidjaya Palembang Sigit Abdurrakhman; Sutijan Sutijan; Muslikhin Hidayat
Jurnal Rekayasa Proses Vol 6 No 2 (2012): Volume 6, Number 2, 2012
Publisher : Jurnal Rekayasa Proses

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.22146/jrekpros.4693

Abstract

Ammonia plant is the main part of fertilizer industry. Primary reformer is an unit operation where catalytic reaction between steam and methane take place, or it is known as steam methane reforming. The main raw material is steam (H2O) and natural gas with major content of methane (CH4). The objective of this research was to develop primary reformer unit process model to calculate temperature, pressure and composition profiles for steady state operation according to operating condition on Ammonia III plant in PT Pupuk Sriwidjaya Palembang.The assumption used was plug flow model both on the furnace side and on the catalytic reactor side for steady state conditions. The ordinary differential equations were solved using Runge Kutta method with Scilab software to get the conversion, pressure and temperature profiles on primary reformer. Variabels evaluated were temperature, pressure, and composition.The simulation result showed that an average error of 3.94 % compared to the operational plant data. For various operating conditions this simulation showed an average error of 7.01 %.
Kinetika reaksi polimerisasi urea-asetaldehid dalam proses enkapsulasi urea Indah Purnamasari; Rochmadi Rochmadi; Hary Sulistyo
Jurnal Rekayasa Proses Vol 6 No 2 (2012): Volume 6, Number 2, 2012
Publisher : Jurnal Rekayasa Proses

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.22146/jrekpros.4694

Abstract

The function of urea encapsulation is to control its release in water, thus increasing effectiveness of using urea and reducing environmental pollution. Microcapsule shell is formed directly on the surface of urea particles called in-situ polymerization. This research aimed to study the kinetics of the polymerization reaction of urea and acetaldehyde in the urea encapsulation process.Urea and acetaldehyde in the ratio of 1:1.2 mol/mol were placed in an erlenmeyer equipped with a thermometer and cooler. The reaction was run for 2 hours in erlenmeyer and sample was taken every 20 minutes. The amount of remaining acetaldehyde was determined by sodium sulfite method and grain size was measured by optical microscope and image pro software. Variables investigated were reaction temperatures (5 - 15°C), particle sizes (14, 18, and 25 mesh), and pH (2 - 4). Reaction rate and diffusivity constants were determined through fitting the experimental data and proposed model.The results showed that the higher temperature and grain size, the higher conversion was. Lower pH (more acid) provides higher conversion but urea particle was seen slightly swelling during the reaction, and also slightly sticky. Addition reaction was much faster than condensation reaction. The proposed reaction kinetics model fitted reasonably well to the experimental data. The process was best conducted at 15°C, 14 mesh, pH 4 and 120 minutes time of reaction which result in 63.38% conversion. Polymer product of urea-acetaldehyde obtained at this condition was slightly harder than that at other conditions.
Studi tekno-ekonomi pemurnian biogas dari limbah domestik Akhwari Wahyu P; Moh Fahrurrozi; Muslikhin Hidayat
Jurnal Rekayasa Proses Vol 6 No 2 (2012): Volume 6, Number 2, 2012
Publisher : Jurnal Rekayasa Proses

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.22146/jrekpros.4695

Abstract

Biogas purification can increase the caloric value of combustion and prevent corrosion. Biogas with 95% of methane is similar to pipeline quality natural gas. The objective of this research was to study technical and economical feasibility of biogas purification and also to estimate gas production cost and scale up capacities.This research used the secondary data from pilot plant of Biogas of Pasar Induk Buah dan Sayuran Gemah Ripah, Gamping, Sleman, Yogyakarta. This research was to obtain the production cost and scale up capacities for each biogas purification method. The sensitivity analysis was conducted to study the influence of gas composition ranged at 30-70% CH4 toward the flow of absorbent to gas ratio, the price of waste changed from decreasing 100% up to increasing 100% and the finance changed ranged at 0-15% to the change of production cost.The result showed that water scrubber was the cheapest method for scrubbing impurities. The production cost of scale up capacities compared to the price of pipeline quality natural gas which ranged at 6-10 US$/MMBtu. The minimum capacity of economical biogas purification methods was 100 tons waste/day. The influence of gas composition ranged at 30-70% of CH4 produced the L/G value change in the absorber column ranged at 0,005-0,025; the influence of waste price from decreasing and up to increasing 100% and finances from 0-15% produced the production cost change ranged at 3-8 US$/MMBtu and 2-14 US$/MMBtu respectively.
Life cycle assessment pabrik semen PT Holcim Indonesia Tbk. pabrik Cilacap: komparasi antara bahan bakar batubara dengan biomassa Taufan Ratri Harjanto; Moh. Fahrurrozi; I Made Bendiyasa
Jurnal Rekayasa Proses Vol 6 No 2 (2012): Volume 6, Number 2, 2012
Publisher : Jurnal Rekayasa Proses

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.22146/jrekpros.4696

Abstract

Holcim Indonesia Tbk. Cilacap having capacity of 2.6 million ton/year uses rice husk as alternative fuels. The utilization of the rice husk will effect the environment. The aim of the study is to evaluate the effects of biomass utilization to environment using life cycle assessment (LCA) method.The “cradle to gate” approach was used to evaluate four scenarios of different fuel combinations: (1) 100% coal, (2) mixed fuel of 90% coal and 10% biomass, (3) mixed fuel of 50% coal and 50% biomass, (4) 100% biomass as primary fuels in the kiln for 1000 kg cement. Evaluation of environment impact related to each scenario was using ISO 14040 (2006) that consists of: (1) goal definition and scoping, (2) inventory analysis, (3) impact assessment, and (4) interpretation.Results showed by contribution analysis, the scenario 1, 2, 3, and 4, give 2.78 x10-1 Pt, 2.24 x10-1Pt, 1.57 x10-1Pt, and 8.50 x10-2 Pt respectively. It was also found that the global warming, respiratory inorganic and resources give significant impacts to the environment. It is suggested to replace silica tranportation using train, to utilize miscanthus giganteus and to grow plants or reforestry.
Karakterisasi dan laju pembakaran biobriket campuran sampah organik dan bungkil jarak (Jatropha curcas L.) Eddy Kurniawan; Wahyudi Budi Sediawan; Muslikhin Hidayat
Jurnal Rekayasa Proses Vol 6 No 2 (2012): Volume 6, Number 2, 2012
Publisher : Jurnal Rekayasa Proses

Show Abstract | Download Original | Original Source | Check in Google Scholar | DOI: 10.22146/jrekpros.4697

Abstract

The potential of biomass municipal waste and jatropha cakes is abundant, but has not been utilized. These materials can be converted into biobriquette via pyrolisis, which can be used as alternative fuel. Tar and tapioca adhesive were applied for the binder.In this study, briquettes with the mass fraction of jatropha cakes of 0, 25, 50, 75 and 100% were used. Research was done by performing carbonization, screening (35 mesh), mixing raw materials (municipal waste, jatropha cakes, tapioca adhesive and tar adhesive) and pressing at 1 kg/cm². Briquettes were then analyzed for compressive strengh, heating value, the moisture content, volatile matter, ash and fixed carbon. The combustion of the briquette was undertaken to study the rate of combustion.Mathematical model showed that the rate of combustion of the briquette with composition of municipal waste and jatropha oil cakes (25% : 75%) with adhesive tar was faster. Briquettes with adhesive tar produce smoke when burned, while briquettes with tapioca adhesive is smoke-free. Therefore it is more preferable. The proposed mathematical model describes the rate of combustion of the briquette well. The kinetic parameter of the rate of combustion were also obtained.

Page 1 of 1 | Total Record : 5


Filter by Year

2012 2012


Filter By Issues
All Issue Vol 19 No 2 (2025): Volume 19, Number 2, 2025 Vol 19 No 1 (2025): Volume 19, Number 1, 2025 Vol 18 No 2 (2024): Volume 18, Number 2, 2024 Vol 18 No 1 (2024): Volume 18, Number 1, 2024 Vol 17 No 2 (2023): Volume 17, Number 2, 2023 Vol 17 No 1 (2023): Volume 17, Number 1, 2023 Vol 16 No 2 (2022): Volume 16, Number 2, 2022 Vol 16 No 1 (2022): Volume 16, Number 1, 2022 Vol 15 No 2 (2021): Volume 15, Number 2, 2021 Vol 15 No 1 (2021): Volume 15, Number 1, 2021 Vol 14 No 2 (2020): Volume 14, Number 2, 2020 Vol 14 No 1 (2020): Volume 14, Number 1, 2020 Vol 13 No 2 (2019): Volume 13, Number 2, 2019 Vol 13 No 1 (2019): Volume 13, Number 1, 2019 Vol 12 No 2 (2018): Volume 12, Number 2, 2018 Vol 12 No 1 (2018): Volume 12, Number 1, 2018 Vol 11 No 2 (2017): Volume 11, Number 2, 2017 Vol 11 No 1 (2017): Volume 11, Number 1, 2017 Vol 10 No 2 (2016): Volume 10, Number 2, 2016 Vol 10 No 1 (2016): Volume 10, Number 1, 2016 Vol 9 No 2 (2015): Volume 9, Number 2, 2015 Vol 9 No 1 (2015): Volume 9, Number 1, 2015 Vol 8 No 2 (2014): Volume 8, Number 2, 2014 Vol 8 No 1 (2014): Volume 8, Number 1, 2014 Vol 7 No 2 (2013): Volume 7, Number 2, 2013 Vol 7 No 1 (2013): Volume 7, Number 1, 2013 Vol 6 No 2 (2012): Volume 6, Number 2, 2012 Vol 6 No 1 (2012): Volume 6, Number 1, 2012 Vol 5 No 2 (2011): Volume 5, Number 2, 2011 Vol 5 No 1 (2011): Volume 5, Number 1, 2011 Vol 4 No 2 (2010): Volume 4, Number 2, 2010 Vol 4 No 1 (2010): Volume 4, Number 1, 2010 Vol 3 No 2 (2009): Volume 3, Number 2, 2009 Vol 3 No 1 (2009): Volume 3, Number 1, 2009 Vol 2 No 2 (2008): Volume 2, Number 2, 2008 Vol 2 No 1 (2008): Volume 2, Nomor 1, 2008 Vol 1 No 1 (2007): Volume 1, Number 1, 2007 More Issue